JPH0665028B2 - Method for manufacturing battery electrode - Google Patents
Method for manufacturing battery electrodeInfo
- Publication number
- JPH0665028B2 JPH0665028B2 JP62235704A JP23570487A JPH0665028B2 JP H0665028 B2 JPH0665028 B2 JP H0665028B2 JP 62235704 A JP62235704 A JP 62235704A JP 23570487 A JP23570487 A JP 23570487A JP H0665028 B2 JPH0665028 B2 JP H0665028B2
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- dimensional structure
- carbonaceous material
- battery
- hydrocarbons
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
- H01M4/583—Carbonaceous material, e.g. graphite-intercalation compounds or CFx
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/22—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the deposition of inorganic material, other than metallic material
- C23C16/26—Deposition of carbon only
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
- H01M4/0402—Methods of deposition of the material
- H01M4/0421—Methods of deposition of the material involving vapour deposition
- H01M4/0428—Chemical vapour deposition
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/139—Processes of manufacture
- H01M4/1393—Processes of manufacture of electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
- H01M4/583—Carbonaceous material, e.g. graphite-intercalation compounds or CFx
- H01M4/587—Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/96—Carbon-based electrodes
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Electrochemistry (AREA)
- Engineering & Computer Science (AREA)
- Inorganic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Battery Electrode And Active Subsutance (AREA)
Description
【発明の詳細な説明】 <産業上の利用分野> 本発明は、小型化、薄型化指向の各種電気機器の電源に
適した電池用電極の製造方法に関する。TECHNICAL FIELD The present invention relates to a method for manufacturing a battery electrode suitable for a power source of various electric appliances oriented toward miniaturization and thinning.
<従来の技術とその問題点> 従来の電子機器用の電池の電極は、電極活物質に導電材
及び結着剤を加え、よく混練し、この混練物を金属ネッ
トなどの集電体に塗着・成型等することにより得られ
る。この電極を相手極に対しセパレータを介して載置し
て電池構造とすることが広く用いられている。<Prior art and its problems> For electrodes of conventional batteries for electronic devices, a conductive material and a binder are added to an electrode active material, and the mixture is kneaded well, and the kneaded product is applied to a collector such as a metal net. It can be obtained by wearing and molding. It is widely used to mount this electrode on a counter electrode via a separator to form a battery structure.
しかし、この様な方法で作製される電極は、電極活物質
と導電材,集電材との電気的接触が悪く、大きな抵抗成
分を有する欠点があった。また、電極活物質の他に導電
材,結着剤を加える必要があったため電極活物質の量が
制限され、エネルギー密度を減少させる原因となってい
た。また得られた電極の活物質を電池構成前に予め電解
液中で電気化学的操作により導入する充電操作を行う必
要があり、製造工程の複雑化の一原因となっていた。However, the electrode manufactured by such a method has a drawback in that the electrical contact between the electrode active material, the conductive material and the current collector is poor, and the electrode has a large resistance component. Further, since it is necessary to add a conductive material and a binder in addition to the electrode active material, the amount of the electrode active material is limited, which causes a decrease in energy density. Further, it is necessary to perform a charging operation in which the obtained active material of the electrode is introduced by an electrochemical operation in an electrolytic solution in advance before forming a battery, which is one cause of complication of the manufacturing process.
本発明は、かかる状況に鑑みてなされたものであり、本
発明の目的は、特に電極活物質と導電剤,集電体との電
気的接触不良に基づく電池容量低下を招くことなく、か
つ、結着剤等を用いることなく高エネルギー密度化が可
能となり、しかも電池構成前に充電操作を特に行なうこ
となく電池用電極として適用でき、製造工程を簡便化で
き安価に製造できる電池用電極の製造方法を提供するこ
とである。The present invention has been made in view of the above circumstances, and an object of the present invention is to bring about a reduction in battery capacity based on poor electrical contact between an electrode active material, a conductive agent, and a current collector, and, in particular, and It is possible to increase the energy density without using a binder, etc. Moreover, it can be applied as a battery electrode without performing a charging operation before the battery is constructed, and the manufacturing process can be simplified and manufactured at low cost. Is to provide a method.
<問題点を解決するための手段> 本発明に係る電池用電極製造方法は、炭化水素類の低温
熱分解による気相堆積法により三次元構造を有する導電
性基体に炭素質材料を直接堆積し、次に、導電性基体に
直接堆積される該炭素質材料と可逆的にインターカレー
ト、デインターカレートが可能な電荷担体物質を該三次
元構造体へ充填し、次に、該電荷担体物質を充填した該
三次元構造体を圧縮して電極体を成形することを特徴と
する。<Means for Solving Problems> In the method for producing a battery electrode according to the present invention, a carbonaceous material is directly deposited on a conductive substrate having a three-dimensional structure by a vapor deposition method by low temperature pyrolysis of hydrocarbons. Then, the three-dimensional structure is filled with a charge carrier substance capable of reversibly intercalating and deintercalating with the carbonaceous material directly deposited on the conductive substrate, and then the charge carrier is filled. It is characterized in that the three-dimensional structure filled with the substance is compressed to form an electrode body.
本発明に係る電池用電極製造方法において、三次元構造
体を有する導電性基体としては、発泡体状(スポンジ
状)、ウール状、織物状、不織布状、ネット状等のいず
れの形態であっても良く、少なくとも外部より加えられ
る圧力により圧縮されて形状を変えることができる可塑
性を有し、かつ、導電性を有するもの、または導電性を
有する材料で表面を被覆しているものであればよい。In the battery electrode manufacturing method according to the present invention, the conductive substrate having a three-dimensional structure may be in any form such as foam (sponge), wool, woven fabric, non-woven fabric, and net. It may be at least a plastic having a plasticity capable of being changed in shape by being compressed by a pressure applied from the outside and having conductivity, or a surface of which is coated with a material having conductivity. .
本発明に用いる炭素質材料は、炭化水素類の低温熱分解
による気相堆積法により適当な基体上に堆積させること
ができる。このとき、出発原料である炭化水素類として
は、脂肪族炭化水素、芳香族炭化水素、脂環族炭化水素
等のいずれであってもよい。また、これらは、窒素原
子,酸素原子等の各種複素原子を含んでいてもよく、ハ
ロゲン原子、水酸基、スルホン酸基、ニトロ基、ニトロ
ソ基、アミノ基、アゾ基、カルボキシル基等の特性基が
付加または置換されていてもよい。低温熱分解される炭
化水素類は気化され、反応系へ給送され、反応系内で熱
分解される。熱分解される炭化水素類の濃度、及び熱分
解する温度は、出発原料とする炭化水素類により異なる
が、通常、数ミリモルパーセントの濃度及び1000℃
程度以下の温度が適当である。出発原料である炭化水素
類を気化する方法には、アルゴンガスをキャリアガスと
するバブラ法、他に、種々のキャリアガスによるバブラ
法、蒸発法、昇華法等の方法がある。The carbonaceous material used in the present invention can be deposited on a suitable substrate by a vapor deposition method by low temperature pyrolysis of hydrocarbons. At this time, the starting hydrocarbons may be any of aliphatic hydrocarbons, aromatic hydrocarbons, alicyclic hydrocarbons and the like. In addition, these may contain various heteroatoms such as nitrogen atom and oxygen atom, and have a characteristic group such as a halogen atom, a hydroxyl group, a sulfonic acid group, a nitro group, a nitroso group, an amino group, an azo group and a carboxyl group. It may be added or substituted. Hydrocarbons that are pyrolyzed at low temperature are vaporized, fed to the reaction system, and pyrolyzed in the reaction system. The concentration of the hydrocarbons to be pyrolyzed and the temperature to be pyrolyzed differ depending on the hydrocarbons used as the starting material, but usually a concentration of several millimole percent and 1000 ° C.
A temperature below about the above is suitable. As a method of vaporizing hydrocarbons as a starting material, there are a bubbler method using argon gas as a carrier gas, a bubbler method using various carrier gases, an evaporation method, a sublimation method, and the like.
三次元構造体を有する導電性基体上に炭素質材料を堆積
して得られる電極は、該炭素質材料と可逆的にインター
カレートとデインターカレートが可能な電荷担体物質が
担持され、外部より加えられる圧力により圧縮され、成
形される。ここで、該電荷担体物質としては、アルカリ
金属、アルカリ土類金属、希土類金属等のドナー型の物
質、及びハロゲン、ハロゲン化合物、金属酸化物、酸素
酸、水素化物等のアクセプター型の物質の粉末状、フレ
ーク状、液体状、ゾル状、ゲル状等のものを用いること
ができる。また、圧縮は通常ローラー圧延により行なう
ことが実用上好ましいが、プレス成形機、その他の押圧
手段により行なってもよい。電極は圧縮により、三次元
構造体の圧縮限界まで任意に制御でき、この範囲内で意
図する厚みの成形体を適宜得ることができる。An electrode obtained by depositing a carbonaceous material on a conductive substrate having a three-dimensional structure carries a charge carrier substance capable of reversibly intercalating and deintercalating with the carbonaceous material, It is compressed and molded by the applied pressure. Here, as the charge carrier substance, a powder of a donor type substance such as an alkali metal, an alkaline earth metal or a rare earth metal, and an acceptor type substance such as a halogen, a halogen compound, a metal oxide, an oxygen acid or a hydride. Shapes, flakes, liquids, sols, gels and the like can be used. Although it is practically preferable to carry out the compression by roller rolling, it may be carried out by a press molding machine or other pressing means. The electrode can be arbitrarily controlled up to the compression limit of the three-dimensional structure by compression, and a molded product having an intended thickness within this range can be appropriately obtained.
この様にして本発明の製造方法で得ることのできる電極
は、非水電解質溶液を電解液とする非水電解液電池、非
水固体電解質を用いる非水固体電解質電池、水溶液を電
解液とするアルカリ電池、酸電池、燃料電池、及び固体
電解質電池等の各種電池の電極として用いることができ
る。In this way, the electrode that can be obtained by the manufacturing method of the present invention is a non-aqueous electrolyte battery using a non-aqueous electrolyte solution as an electrolytic solution, a non-aqueous solid electrolyte battery using a non-aqueous solid electrolyte, and an aqueous solution as an electrolytic solution. It can be used as an electrode for various batteries such as alkaline batteries, acid batteries, fuel cells, and solid electrolyte batteries.
<作用> 本発明によれば、炭化水素類の低温熱分解で三次元構造
を有する導電性基体材料上に炭素質材料を気相より直接
堆積して得られる電極に、該炭素質材料と可逆的にイン
ターカレート,デインターカレート可能な電荷担体物質
を担持し、かつこれらの該三次元構造体の圧縮により形
成されて電池用電極を得ることができる。<Operation> According to the present invention, an electrode obtained by directly depositing a carbonaceous material from a vapor phase on a conductive substrate material having a three-dimensional structure by low-temperature pyrolysis of hydrocarbons is reversible with the carbonaceous material. It is possible to obtain a battery electrode by carrying a charge carrier substance which can be intercalated and deintercalated, and formed by compression of these three-dimensional structures.
電極活物質である炭素質材料を電荷集電体である導電性
基体に直接堆積し、電気的、機械的に連結されるので、
結着剤や導電剤が不要であり、高容量化が可能になる。
さらに、電荷担体物質が炭素質材料に担持されるので、
電池構成前に電極化成処理を施す必要がない。Since the carbonaceous material that is the electrode active material is directly deposited on the conductive substrate that is the charge collector, and electrically and mechanically connected,
No binding agent or conductive agent is required, and high capacity is possible.
Furthermore, since the charge carrier material is supported on the carbonaceous material,
There is no need to perform electrode chemical conversion treatment prior to battery construction.
これは、炭素質材料が電極担体物質と接触しているため
に、電池を作製したとき(電極液に接触したとき)に反
応が起こり層間化合物を形成するからである。This is because the carbonaceous material is in contact with the electrode carrier substance, so that a reaction occurs when a battery is manufactured (when it is in contact with the electrode liquid) to form an intercalation compound.
<発明の効果> 本発明の製造方法で得られる電極は、高い容量密度を有
し、また長期間にわたる充電・放電の繰り返しによって
劣化しないため、該電極を用いて電池を構成することに
よりエネルギー密度の高い、サイクル寿命の優れた電池
を得ることができる。さらに電極製造の工程において、
活物質等の混練、塗布、乾燥、充電などの繁雑な工程を
省略できるための工程が簡略化でき容易となる。すなわ
ち、本発明の製造方法により、高い容量密度を有し、さ
らにサイクル寿命の優れた電極が提供でき、かつ製造工
程の簡略化、短縮化が可能となるため、本発明製造方法
により特性の優れた、しかも安価な電極を得ることがで
き、その工業的価値は極めて大きい。<Effects of the Invention> The electrode obtained by the production method of the present invention has a high capacity density and does not deteriorate due to repeated charging / discharging over a long period of time. Therefore, by constructing a battery using the electrode, the energy density can be improved. It is possible to obtain a battery having a high cycle life and an excellent cycle life. Furthermore, in the electrode manufacturing process,
Since the complicated steps such as kneading, coating, drying and charging of the active material can be omitted, the steps can be simplified and facilitated. That is, since the manufacturing method of the present invention can provide an electrode having a high capacity density and an excellent cycle life, and can simplify and shorten the manufacturing process, the manufacturing method of the present invention has excellent characteristics. Moreover, an inexpensive electrode can be obtained, and its industrial value is extremely large.
<実施例> 以下実施例により本発明をさらに詳細に説明する。尚、
本発明は以下の実施例で制限されるものではない。<Examples> The present invention will be described in more detail with reference to Examples. still,
The present invention is not limited to the following examples.
三次元構造を有する導電性基体上に堆積される炭素質材
料は、第1図の反応装置を用い形成した。すなわち、一
旦、脱水処理を施し、さらに真空移送による蒸留精製操
作を行なったベンゼンを収納したバブル容器1内にアル
ゴンガス供給器2よりアルゴンガスを供給し、ベンゼン
のバブルを行なう。そして、パイレックス製ガラス管3
を介し、石英製反応管4へベンゼンを給送した。このと
き、容器1をベンゼンの蒸発による吸熱分だけ加熱する
ことにより温度を一定に保ち、また、ニードル弁5,6
によりベンゼン量を最適化した。反応管4には厚さ約1.
5mmの発泡状ニッケル板よりなる三次元構造を有する導
電性基体の載置されたホルダー7が設置され反応管4の
外周囲には加熱炉8が周設されている。この加熱炉8に
よりホルダー7及び、発泡性ニッケル板を約1000℃
に維持し、パイレックス製ガラス管3より供給されるベ
ンゼンを熱分解し、約60分間炭素質材料を発泡性ニッ
ケル板7上に堆積させた。熱分解後に、反応管4内に残
留するガスは、排気設備9,10を介して除去した。The carbonaceous material deposited on the conductive substrate having a three-dimensional structure was formed by using the reactor shown in FIG. That is, argon gas is supplied from an argon gas supplier 2 into a bubble container 1 containing benzene which has been dehydrated and then subjected to a distillation and purification operation by vacuum transfer to bubble benzene. And Pyrex glass tube 3
Benzene was fed to the quartz reaction tube 4 via the. At this time, the temperature of the container 1 is kept constant by heating the container 1 by the amount of heat absorbed by the evaporation of benzene.
The amount of benzene was optimized by The reaction tube 4 has a thickness of about 1.
A holder 7 on which a conductive substrate having a three-dimensional structure made of a foamed nickel plate of 5 mm is placed is installed, and a heating furnace 8 is provided around the outer periphery of the reaction tube 4. With this heating furnace 8, the holder 7 and the foamable nickel plate are heated to about 1000 ° C.
Benzene supplied from the Pyrex glass tube 3 was pyrolyzed and the carbonaceous material was deposited on the foamable nickel plate 7 for about 60 minutes. After the thermal decomposition, the gas remaining in the reaction tube 4 was removed through the exhaust equipment 9 and 10.
この方法により該炭素質材料を、堆積させた三次元構造
を有する導電性基体に140メッシュパスのリチウム金
属粉末を所定量充填し、次にローラー圧延機によりロー
ラー圧延を行ない、厚さ0.2mmに成形された電極を得
た。第2図は電極11をローラー12,12で圧延して
いる斜視図である。充填されたリチウム粉末の量は、該
炭素質材料が、吸収可能な量に制限されており、後で説
明する電極の化成の後にリチウム金属粉末が未反応物と
して残存することはなかった。According to this method, the conductive base material having a three-dimensional structure deposited by this method is filled with a predetermined amount of lithium metal powder having a 140 mesh path, and then roller rolling is performed by a roller rolling machine to obtain a thickness of 0.2 mm. A molded electrode was obtained. FIG. 2 is a perspective view in which the electrode 11 is rolled by the rollers 12, 12. The amount of the charged lithium powder was limited to the amount that the carbonaceous material could absorb, and the lithium metal powder did not remain as an unreacted material after the formation of the electrode, which will be described later.
以上の様にしてリチウム金属粉末と共にローラー圧延に
より圧縮成型して得られた薄板状電極体を1Mの過塩素
酸リチウムを溶質として含むプロピレンボネート溶液の
入った電解槽に浸漬し、粉末状の金属リチウムを該炭素
質材料中に吸収させ電極の化成を行なった。化成済の電
極を電解槽より取り出し、電解質溶液を充分に取り除い
た後に、所定の形状に切断して本発明の電極を得た。The thin plate-like electrode body obtained by compression-molding with the lithium metal powder by the roller rolling as described above is immersed in an electrolytic cell containing a propylene carbonate solution containing 1M lithium perchlorate as a solute to obtain a powdery metal. The electrodes were formed by absorbing lithium in the carbonaceous material. The chemically formed electrode was taken out of the electrolytic cell, and after sufficiently removing the electrolyte solution, it was cut into a predetermined shape to obtain an electrode of the present invention.
なお、本実施例では、電極の化成を行ったが、電荷担体
物質である金属リチウムが炭素質材料に担持されている
ので、先に説明したように、電池構成の前に電極化成処
理を特に施さなくてもよい。これにより、製造工程を簡
素化できる。Incidentally, in the present example, the formation of the electrode was performed, but since the metallic lithium, which is the charge carrier substance, is supported on the carbonaceous material, as described above, the electrode formation treatment is particularly performed before the battery configuration. It does not have to be applied. Thereby, the manufacturing process can be simplified.
上記の方法で作製した電極について、1M過塩素酸リチ
ウムを溶質として含むプロピレンカーボネート溶液中に
浸し、一夜放置したところ、リチウム電極に対し30mV
の電位を示した。またリチウム電極に対し2.5Vまで放
電したところ、該炭素質材料1gに対し320mAhの放
電容量を得た。すなわち、本発明の電極が、リチウム金
属粉末を効率良く吸収していたことがわかった。さら
に、サイクル寿命を調べる目的でリチウム電極に対し、
0Vまで充電し、2.5Vまで放電する充放電サイクルを
繰り返したところ、200回以上を繰り返しても放電電
気量の低下はほとんどみられなかった。The electrode produced by the above method was immersed in a propylene carbonate solution containing 1M lithium perchlorate as a solute and left overnight, and the result was 30 mV to the lithium electrode.
The potential of When the lithium electrode was discharged to 2.5 V, a discharge capacity of 320 mAh was obtained for 1 g of the carbonaceous material. That is, it was found that the electrode of the present invention efficiently absorbed the lithium metal powder. Furthermore, for the purpose of examining the cycle life, for lithium electrodes,
When the charge / discharge cycle of charging to 0 V and discharging to 2.5 V was repeated, the amount of discharged electricity was hardly decreased even after repeating 200 times or more.
第1図は、本発明における一工程に用いる炭素質材料堆
積装置の構成説明図である。 第2図は、本発明におけるローラー圧延する工程を示す
斜視図である。FIG. 1 is a configuration explanatory view of a carbonaceous material deposition apparatus used for one step in the present invention. FIG. 2 is a perspective view showing a roller rolling process in the present invention.
Claims (1)
により三次元構造を有する導電性基体に炭素質材料を直
接堆積し、 次に、導電性基体に直接堆積される該炭素質材料と可逆
的にインターカレート、デインターカレートが可能な電
荷担体物質を該三次元構造体へ充填し、 次に、該電荷担体物質を充填した該三次元構造体を圧縮
して電極体を成形することを特徴とする電池用電極の製
造方法。1. A carbonaceous material directly deposited on a conductive substrate having a three-dimensional structure by a vapor deposition method by low-temperature pyrolysis of hydrocarbons, and then directly deposited on the conductive substrate. The charge carrier substance capable of reversibly intercalating and deintercalating is filled in the three-dimensional structure, and the three-dimensional structure filled with the charge carrier substance is compressed to form an electrode body. A method for manufacturing a battery electrode, which comprises molding.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62235704A JPH0665028B2 (en) | 1987-09-19 | 1987-09-19 | Method for manufacturing battery electrode |
| EP88308628A EP0309171B1 (en) | 1987-09-19 | 1988-09-16 | A method for the production of a carbon electrode |
| DE8888308628T DE3871684T2 (en) | 1987-09-19 | 1988-09-16 | METHOD FOR PRODUCING A CARBON ELECTRODE. |
| US07/245,772 US4931240A (en) | 1987-09-19 | 1988-09-19 | Method for the production of a carbon electrode |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62235704A JPH0665028B2 (en) | 1987-09-19 | 1987-09-19 | Method for manufacturing battery electrode |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6481167A JPS6481167A (en) | 1989-03-27 |
| JPH0665028B2 true JPH0665028B2 (en) | 1994-08-22 |
Family
ID=16989992
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62235704A Expired - Fee Related JPH0665028B2 (en) | 1987-09-19 | 1987-09-19 | Method for manufacturing battery electrode |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US4931240A (en) |
| EP (1) | EP0309171B1 (en) |
| JP (1) | JPH0665028B2 (en) |
| DE (1) | DE3871684T2 (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0815074B2 (en) * | 1986-11-11 | 1996-02-14 | シャープ株式会社 | Method for manufacturing carbon body electrode |
| JPH06163080A (en) * | 1992-11-19 | 1994-06-10 | Sanyo Electric Co Ltd | Secondary battery |
| US5601949A (en) * | 1992-11-19 | 1997-02-11 | Sanyo Electric Co., Ltd. | Ion conductive material for secondary battery |
| US5601950A (en) * | 1994-06-29 | 1997-02-11 | Sony Corporation | Non-aqueous electrolyte secondary cell |
| US8524397B1 (en) | 2004-11-08 | 2013-09-03 | Quallion Llc | Battery having high rate and high capacity capabilities |
| US7052802B2 (en) * | 2002-10-15 | 2006-05-30 | Quallion Llc | Fluorinated carbon active material |
| WO2005006469A1 (en) * | 2003-07-15 | 2005-01-20 | Itochu Corporation | Current collecting structure and electrode structure |
| US20050130043A1 (en) * | 2003-07-29 | 2005-06-16 | Yuan Gao | Lithium metal dispersion in electrodes |
| JP4911909B2 (en) * | 2005-03-29 | 2012-04-04 | 三洋電機株式会社 | Method for producing electrode for lithium secondary battery |
| US7754390B2 (en) * | 2006-03-14 | 2010-07-13 | Panasonic Corporation | Manufacturing method of negative electrode for nonaqueous electrolytic rechargeable battery, and nonaqueous electrolytic rechargeable battery using it |
Family Cites Families (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1163979A (en) * | 1967-03-07 | 1969-09-10 | Ducommmun Inc | Reinforced Composite Materials |
| US3647511A (en) * | 1969-03-20 | 1972-03-07 | Gen Electric | Method of preparing curved pyrolytic graphite bodies having increased thickness to radius ratios |
| US3949106A (en) * | 1969-12-29 | 1976-04-06 | Toyo Boseki Kabushiki Kaisha | Method for producing isotropic pyrolisis carbon coatings |
| US3895084A (en) * | 1972-03-28 | 1975-07-15 | Ducommun Inc | Fiber reinforced composite product |
| JPS49104143A (en) * | 1973-01-22 | 1974-10-02 | ||
| US3944686A (en) * | 1974-06-19 | 1976-03-16 | Pfizer Inc. | Method for vapor depositing pyrolytic carbon on porous sheets of carbon material |
| US4178413A (en) * | 1977-10-03 | 1979-12-11 | The Carborundum Company | Fiber reinforced carbon and graphite articles and a method of producing said articles |
| US4396663A (en) * | 1979-06-11 | 1983-08-02 | The B. F. Goodrich Company | Carbon composite article and method of making same |
| US4318948A (en) * | 1979-07-25 | 1982-03-09 | Fordath Limited | Article comprising carbon fibres and method of producing the article |
| JPS59154763A (en) * | 1983-02-22 | 1984-09-03 | Sanyo Chem Ind Ltd | Negative pole material for lithic secondary cell |
| JPS6036315A (en) * | 1983-08-10 | 1985-02-25 | Toray Ind Inc | Carbon fiber structure and secondary battery using it |
| JPS617567A (en) * | 1984-06-22 | 1986-01-14 | Hitachi Ltd | Secondary battery and its manufacturing method |
-
1987
- 1987-09-19 JP JP62235704A patent/JPH0665028B2/en not_active Expired - Fee Related
-
1988
- 1988-09-16 EP EP88308628A patent/EP0309171B1/en not_active Expired - Lifetime
- 1988-09-16 DE DE8888308628T patent/DE3871684T2/en not_active Expired - Lifetime
- 1988-09-19 US US07/245,772 patent/US4931240A/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| EP0309171B1 (en) | 1992-06-03 |
| US4931240A (en) | 1990-06-05 |
| DE3871684D1 (en) | 1992-07-09 |
| EP0309171A1 (en) | 1989-03-29 |
| JPS6481167A (en) | 1989-03-27 |
| DE3871684T2 (en) | 1992-12-17 |
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